CN206778702U - A kind of regulating temperature and humidity sieves electric cleaner - Google Patents

A kind of regulating temperature and humidity sieves electric cleaner Download PDF

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Publication number
CN206778702U
CN206778702U CN201720390941.XU CN201720390941U CN206778702U CN 206778702 U CN206778702 U CN 206778702U CN 201720390941 U CN201720390941 U CN 201720390941U CN 206778702 U CN206778702 U CN 206778702U
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China
Prior art keywords
dust
cathode
anode
flue gas
humidity
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CN201720390941.XU
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Chinese (zh)
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赵海宝
赵锡勇
胡露钧
何毓忠
崔盈
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Zhejiang Feida Environmental Science and Technology Co Ltd
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Zhejiang Feida Environmental Science and Technology Co Ltd
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Abstract

The utility model discloses a kind of regulating temperature and humidity to sieve electric cleaner, including the smoke temperature reducer, flue gas humidity control device and electric dust collector being sequentially connected, along flow of flue gas direction, the electric dust collector includes import loudspeaker, conventional electric field, screening electric field and outlet loudspeaker successively, and water conservancy diversion dust collect plant is provided with the import loudspeaker.The utility model has the advantages that:It can ensure that flue-gas temperature deep-graded cools, dust is modified ratio resistance reduction, adhesion increase improves efficiency of dust collection, is stripped of the higher dust of adhesion, improves dust collection efficiency, realizes that dust classification removes;System particles thing removal efficiency is greatly improved, the stable realization for coal-burning power plant's particulate matter minimum discharge provides precondition;Due to exhaust gas dust adhesion increase after flue gas water spray damping, efficiency of dust collection effectively improves;Realize while adjust electric cleaner import smoke moisture and temperature to improve dust collection efficiency, reduce energy consumption.

Description

A kind of regulating temperature and humidity sieves electric cleaner
Technical field
It the utility model is related to a kind of regulating temperature and humidity screening electric cleaner.
Background technology
The particulate matter of coal-burning power plant's discharge includes PM2.5A fine grained, condensable particle and droplet containing soluble salt, be One of major reason of serious gray haze in recent years is caused, it is substantially full with implementing in full for coal-burning power plant of China minimum discharge Foot-powder dirt emission request, but conventional dry electric cleaner can not still realize 10mg/m under the conditions of low energy consumption3Following stable row Put.
Existing electric cleaner has following defect:
1. existing electrostatic precipitator typically matches somebody with somebody pattern, pole plate arrangement and flue gas stream direction using the pole of " pole plate-polar curve " Parallel, this structure has that reentrainment of dust is obvious, dust needs enough migration velocitys to pass perpendicularly through flue gas to be adsorbed onto on positive plate The problems such as.
2. existing electric cleaner does not account for adjusting electric cleaner import smoke moisture and temperature simultaneously to improve electric precipitation Efficiency, reduce energy consumption.
3. flue-gas temperature is simply reduced to 90 DEG C or so by existing low temperature electric cleaner, that flue-gas temperature is not further 80 DEG C or so are reduced to, further to improve dust collection efficiency, reduces energy consumption.
For the negative electrode of 4 existing electric cleaners typically using linear, individual cathode structure uses the auxiliary electrode of plate shape, palette with Flue gas direction is parallel, does not play a part of dust;
5. its guide functions of the deflector of existing electric cleaner import loudspeaker, effect of not gathering dust;
Desulfurization wastewater is simply directly sprayed onto electric cleaner front end smoke canal by 6 existing " desulfurization wastewater zero-emissions ", electricity is present and is removed Dirt device airflow-distribution board because the reasons such as humidity increase, waste water saliferous cause dust stratification serious the problem of, and desulfurization wastewater spray into system System lacks on-bne repair maintenance system, blockage problem be present.
7. existing dedusting technology can not effectively remove condensable particle and droplet containing soluble salt.
Utility model content
The purpose of this utility model is that providing a kind of regulating temperature and humidity sieves electric cleaner, can effectively solve the problem that existing dedusting The problem of device efficiency is low, high energy consumption.
In order to solve the above-mentioned technical problem, the utility model is achieved through the following technical solutions:A kind of regulating temperature and humidity Electric cleaner, including smoke temperature reducer, flue gas humidity control device and the electric dust collector being sequentially connected are sieved, along flow of flue gas side To the electric dust collector includes import loudspeaker, conventional electric field, sieves electric field and outlet loudspeaker successively, in the import loudspeaker Provided with water conservancy diversion dust collect plant.
Preferably, four cathode hangers are equipped with each import loudspeaker, four cathode hangers connect one High voltage power supply;The conventional electric field includes at least one electric precipitation room, and four cathode hangers are provided with each electric precipitation room, described Four cathode hangers connect a high voltage power supply;The screening electric field includes at least one screening electric precipitation room, each sieve Divide in electric precipitation room and be provided with eight cathode hangers, eight cathode hangers connect a high voltage power supply;Multizone is independently-powered, Ensure regional powered stable, be advantageous to stablize ramping effect.
Preferably, it is described screening electric field include negative electrode and anode, the negative electrode and anode are steel wire, the negative electrode with Anode is vertical with flue gas flow direction;Negative electrode and anode are passed perpendicularly through by the flue gas for sieving electric field, avoid rapping reentrainment of dust, Effectively increase dust migration velocity.
Preferably, the negative electrode is provided with some corona pins, and the corona pin includes screw and nut, and the tip of screw is remote From negative electrode, the afterbody of screw is fixed on negative electrode by nut;Using screw head point discharge, manufacturing cost is reduced, is not had to Go specially to design corona pin again, and it is all very convenient by nut fixation handling maintenance.
Preferably, the spacing of the negative electrode and anode is 400-500mm, and steel wire net height is 2000mm, and steel wire is wide Degree is 1000mm, is 8mm × 8mm square hole on steel wire;The spacing of negative electrode and anode ensures the spacing of optimal dust removing effects, The height or width of steel wire are crossed conference and are easily deformed, and size is too small not economical enough.
Preferably, in the screening electric field negative electrode of each power supply zone by framework composition together, the anode Often row is independent into one group;Negative electrode and anode is allowed to play maximum effect.
Preferably, the water conservancy diversion dust collect plant includes deflector, anode dust-collecting mechanism and negative electrode dust-collecting mechanism, by flue gas stream Dynamic direction, the deflector are located at the upstream of anode dust-collecting mechanism and negative electrode dust-collecting mechanism;Water conservancy diversion first is carried out to the flue gas of entrance, First time dust is carried out again, removes the big dust of adhesion.
Preferably, the negative electrode dust-collecting mechanism includes cathode frame, cathode rapping axle and cathode rapping motor, the negative electrode Cathode line or negative electrode steel wire are provided with framework, cathode frame top is often arranged and is hung over by insulated hanging pole in import loudspeaker, phase The bottom of adjacent cathode frame is fixedly connected, and position corresponding with often arranging cathode frame is provided with beater on cathode rapping axle, described Cathode rapping axle is connected with cathode rapping motor, and the cathode rapping motor is fixed on the top of import loudspeaker;Cathode frame is all Link together, shorten the rapping time.
Preferably, the anode dust-collecting mechanism includes anodic porous plate and cathode vibrator, two adjacent row's negative electrode frames Anodic porous plate described in a row is provided between frame, the level height of the anodic porous plate bottom is more than the water of cathode frame bottom Flat height, cathode vibrator include anode electric motor of shaker and anode rapping shaft, on anode rapping shaft with often row's anodic porous plate Corresponding position is provided with beater, and the anode rapping shaft is connected with anode electric motor of shaker, and the anode electric motor of shaker is fixed on The bottom of import loudspeaker;Dust is more, it is necessary to which independent rapping, ensures ramping effect on anodic porous plate.
Preferably, the left and right sides of the anodic porous plate is provided with the bevelling that flue gas is imported to anodic porous plate, the sun Equally distributed through hole is provided with the porous plate of pole, both sides are angled so that flue gas water conservancy diversion, through hole then ensure flue gas normal stream It is logical, make flue gas as far as possible uniformly through each through hole.
Preferably, it is equipped with the deflector, anode dust-collecting mechanism and negative electrode dust-collecting mechanism and spreads flue gas to surrounding Flow distribution plate, so as to ensure that the air-flow in conventional electric field is uniform.
Preferably, the flue gas humidity control device includes the water-supply-pipe being arranged in flue, and the end of the water-supply-pipe is provided with Nozzle, the nozzle height are staggered, and nozzle ejection flow direction is reversely consistent with flow of flue gas, and the waste water of penetrating is with cigarette Gas together spreads.
Preferably, the water-supply-pipe windward side is provided with abrasionproof angle steel, avoids causing because high concentrate dust washes away water-supply-pipe Abrasion leakage.
Preferably, connected between the water-supply-pipe and water inlet manifold by transparent hose, the both ends of the transparent hose are equal Provided with stop valve, each pipeline water delivery performance is observed in realization online, and realizes on-bne repair and maintenance.
Preferably, dust collection plate is provided with the outlet loudspeaker, the dust collection plate includes plate body, and the left and right sides of plate body is provided with Towards the first side plate of flue gas upstream, the front end of every block of first side plate is provided with the side plate of plate body center second, two piece of second side Fume inlet passage is left between plate, both sides form frame-shaped construction, the powered ultrafine dust in part of absorption screening electric field escape.
Compared with prior art, the utility model has the advantages that:Can be with by smoke temperature reducer and flue gas humidity control device Ensure the cooling of flue-gas temperature deep-graded, dust is modified ratio resistance reduction, adhesion increase improves efficiency of dust collection, passes through import loudspeaker The water conservancy diversion integrating device that place is set be stripped of because smoke temperature reducer and flue gas humidity control device are set and caused by adhesion compared with High dust, dust collection efficiency is improved, then coordinated with electric dust collector, realize that dust classification removes;
Flue gas is down to 80 DEG C by smoke temperature reducer and flue gas humidity control device, effectively by the SO in flue gas3Condensation product Dew, and neutralized by dust surface alkalinty oxide, it is stripped of downstream (NH4)2SO4The reactant SO of formation3, so that coal-fired electricity The important component SO of factory's flue gas particles discharge3(condensable particulate matter) and (NH4)2SO4(droplet containing soluble salt) obtains Effectively remove, greatly improve system particles thing removal efficiency, the stable realization for coal-burning power plant's particulate matter minimum discharge provides Precondition;
Due to exhaust gas dust adhesion increase after flue gas water spray damping, efficiency of dust collection effectively improves;Realize simultaneously Regulation electric cleaner import smoke moisture and temperature reduce energy consumption to improve dust collection efficiency.
Brief description of the drawings
Fig. 1 is the structural representation that a kind of regulating temperature and humidity of the utility model sieves electric cleaner;
Fig. 2 be Fig. 1 in A to structural representation;
Fig. 3 is the structural representation that a kind of regulating temperature and humidity of the utility model sieves import loudspeaker in electric cleaner;
Fig. 4 is partial enlarged drawing at D in Fig. 3;
Fig. 5 is the structural representation that a kind of regulating temperature and humidity of the utility model sieves electric cleaner Anodic deflector;
Fig. 6 is C-C sectional views in Fig. 5;
Fig. 7 is B-B sectional views in Fig. 1;
Fig. 8 is that a kind of regulating temperature and humidity of the utility model sieves the solid that electric field negative pole part and anode portion are sieved in electric cleaner Figure;
Fig. 9 is that a kind of regulating temperature and humidity of the utility model sieves screening electric field flue gas flow direction schematic diagram in electric cleaner;
Figure 10 is that the flow of flue gas that a kind of regulating temperature and humidity of the utility model is sieved in electric cleaner in electric dust collector is illustrated Figure;
Figure 11 is that a kind of regulating temperature and humidity of the utility model sieves plate structure schematic diagram of being gathered dust in electric cleaner;
Figure 12 is F-F sectional views in Figure 10.
Arrow in above-mentioned figure is flow of flue gas direction.
Embodiment
It is the embodiment that a kind of regulating temperature and humidity of the utility model sieves electric cleaner refering to Fig. 1, a kind of regulating temperature and humidity screening Electric cleaner, including smoke temperature reducer 1, flue gas humidity control device 2, import loudspeaker 3, conventional electric field 4, the screening electricity being sequentially connected Field 5 and outlet loudspeaker 6.
As shown in Fig. 2 flue gas humidity control device 2 includes the water-supply-pipe 23 being arranged in flue 22, the end of the water-supply-pipe 23 Portion is provided with nozzle 24, and the height of nozzle 24, left and right are staggered, and nozzle 24 sprays flow direction and flow of flue gas reverse one Cause, the waste water of penetrating together spreads with flue gas, and the windward side of water-supply-pipe 23 is provided with abrasionproof angle steel, avoids because high concentrate dust washes away Water-supply-pipe 23 and cause abrasion to be revealed, and water-supply-pipe 23 use stainless steel, to reduce corrosion, raising service life.
In the upside of flue 22, U-shaped transparent hose 27,27 liang of transparent hose are set between each water-supply-pipe 23 and water inlet manifold Side sets hand stop valve 28, and each pipeline water delivery performance is observed in realization online, and realizes on-bne repair and maintenance.
As shown in figure 3, being provided with water conservancy diversion dust collect plant 7 in the import loudspeaker 3, the water conservancy diversion dust collect plant 7 includes water conservancy diversion Plate 12, anode dust-collecting mechanism and negative electrode dust-collecting mechanism, by flow of flue gas direction, the deflector 12 be located at anode dust-collecting mechanism and The upstream of negative electrode dust-collecting mechanism, anode dust-collecting mechanism include anodic porous plate 16 and cathode vibrator, negative electrode dust-collecting mechanism bag Cathode frame 13, cathode rapping axle 14 and cathode rapping motor 15 are included, cathode line or negative electrode are provided with the cathode frame 13 Steel wire.
Arrangement two is discharged to four row's anodic porous plates 16 and cathode line or negative electrode steel wire in import loudspeaker 3, and negative electrode is towards side Prominent, cathode rapping motor 15 is reducing motor, drives cathode rapping axle 14 to rotate, and cathode rapping axle 14 is corresponding often to arrange negative electrode frame The position of frame 13 sets beater, so as to rotate rapping cathode frame 13 by row by beater, removes absorption on negative electrode Dust, anode dust-collecting mechanism include anodic porous plate 16 and cathode vibrator, are provided between two adjacent row's cathode frames 13 Anodic porous plate 16 described in one row, the level height of the bottom of anodic porous plate 16 are more than the level height of the bottom of cathode frame 13 Degree, cathode vibrator include anode electric motor of shaker 17 and anode rapping shaft 18, arrange on anode rapping shaft 18 and often anodic porous Position corresponding to plate 16 is provided with beater, and the anode rapping shaft 18 is connected with anode electric motor of shaker 17, the anode rapping electricity Machine 17 is fixed on the bottom of import loudspeaker 3.
In negative electrode integrated mechanism, the upper and lower frames of negative electrode is connected as integral frame structure, above passes through four insulated hanging pole branch Support, cathode rapping motor 15 are arranged on the top of import loudspeaker 3;Anodic porous plate 16 in anode dust-collecting mechanism, often row is independent, on End suspension is fixed, and bottom staggered by shortening length with cathode frame 13, cathode vibrator rapping anode flow field 12 by row, Absorption and the dust sticked are removed in rapping, and dust is squeezed into electric field ash bucket.
As shown in Figure 5, Figure 6, the thickness 2.5mm-3.5mm of anode flow field 12, width about 360mm, using wear-resisting Q345 Material, equally distributed through hole 20, the opening diameter φ 85mm of through hole 20, the section of anode flow field 12 are provided with anodic porous plate 16 Such as channel steel type, the left and right sides is provided with the bevelling 19 that flue gas is imported to anodic porous plate 16, both sides bevelling 19 it is angled so as to Flue gas water conservancy diversion.
As shown in figure 4, arrow is flow of flue gas direction in figure, deflector 12, anode dust-collecting mechanism and negative electrode dust-collecting mechanism On be equipped with the flow distribution plate 21 for spreading flue gas to surrounding, so as to ensure that the air-flow in conventional electric field 4 is uniform.
As shown in Figure 7, Figure 8, screening electric field 5 includes negative pole part 8 and anode portion 9, and negative pole part 8 and anode portion 9 are steel wire Net, below in order to distinguish referred to as negative electrode steel wire and anode steel wire, but their basic structures are consistent, with conventional electric cleaner Positive plate it is different from flue gas parallel arrangement, the negative pole part 8 of the present apparatus and the steel wire of anode portion 9 are vertical with flue gas flow direction, cigarette Gas needs guiding through the aperture of steel wire, and flue gas passes perpendicularly through anode steel wire, improves migration velocity, and negative electrode uses steel wire, flue gas Also pass perpendicularly through negative electrode steel wire, this avoid rapping reentrainment of dust, dust under airflow function with anode steel wire low coverage From contact, dust migration velocity is effectively increased.
As shown in figure 9, setting some corona pins 10 on negative electrode steel wire, corona pin 10 includes screw and nut, screw Tip be fixed on away from negative electrode, the afterbody of screw by nut on negative electrode, negative electrode steel wire access high-tension electricity, pass through screw Tip produces corona so that the dust charged flowed vertically to, and vertically as flue gas flow direction enters anode steel wire, in coulomb In the presence of power, inertia, it is adsorbed onto on anode steel wire and negative electrode steel wire, negative electrode steel wire also achieves integrated effect, By rapping apparatus by dust it is blocking squeeze into downside ash bucket in, so as to remove chalk dust removing.
The distance of negative electrode steel wire and anode steel wire is typically in 400mm-500mm, negative electrode steel wire and anode steel wire The each separate unit of framework be generally 2000mm height × 1000 width, framework is square tube, and steel wire is fixed with framework, steel wire The steel wire of net is φ 0.63mm, and steel wire space is 8mm × 8mm square hole, and steel wire uses stainless steel wire, and generally 304 is stainless Steel or 316 stainless steels.
The negative electrode of the either each room of screening 5 each power supply zone of electric field is combined entirely through frame structure, is led to Cross rapping apparatus entirety rapping cathode assembly;Anode steel wire is combined by frame structure, anode superstructure often arrange it is independently combinable into One group, pass through rapping apparatus rapping anode superstructure by row.
As shown in Figure 10, whole electric dust collector includes import loudspeaker 3, conventional electric field 4, screening electric field 5 and outlet successively Loudspeaker 6, are provided with high voltage power supply device in electric dust collector, each import loudspeaker 3 of water conservancy diversion dust collect plant 7 be independently arranged it is a set of, often Set sets four cathode hangers, and independently-powered, and high voltage power supply is arranged at the top of the first electric field, and 4 each room of conventional electric field is set Four cathode hangers, a supporting power supply are put, 5 each room of screening electric field sets eight cathode hangers, a supporting power supply Power supply;Each room is divided into two subregions by screening electric field 5, and power supply, supporting two rapping apparatus, to carry are connected with wire 11 The ash-removal effect of high rapping apparatus.
As shown in Figure 11, Figure 12, dust collection plate 29 is provided with outlet loudspeaker 6, the dust collection plate 29 includes plate body 30, plate body 30 The left and right sides be provided with the first side plate 31 of flue gas upstream, the front end of every block of first side plate 31 is provided with the center of plate body 30 Second side plate 32, fume inlet passage 33 is left between two piece of second side plate 32, both sides form frame-shaped construction, and absorption screening electric field 5 is escaped The powered ultrafine dust in part of ease.
Flue-gas temperature is reduced to 83-85 DEG C or so by smoke temperature reducer;Flue gas humidity control device 2 is arranged in flue gas cool-down dress Before postponing electric cleaner suction flange, desulfurization wastewater or wet electrical dust precipitator waste water are sprayed into flue, by spraying water flue gas Temperature is further decreased to 80 DEG C in flue, avoids smoke temperature reducer etching problem caused by cooling;Water injection system On-bne repair can be realized by transparent hose;The water conservancy diversion dust collect plant 7 of import loudspeaker 3 sets negative electrode charge device, and porous plate is simultaneously Possess water conservancy diversion and the effect gathered dust, and corresponding ash removal equipment for flapping is set, while can effectively avoid because flue gas cool-down is humidified The problem of caused dust is attached to deflector 12 and causes blocking afterwards;Screening electric field 5 is arranged in electric cleaner rear end electric field, sun Extremely steel wire, anode network are arranged vertically with flue gas, and flue gas passes perpendicularly through anode steel wire, improve migration velocity;Negative electrode uses Steel wire, sets the point discharge pin of screw shaped on steel wire, and flue gas passes perpendicularly through negative electrode steel wire;Flue gas need to pass perpendicularly through Multilayer steel wire, avoids rapping reentrainment of dust, and dust, with anode network close contact, effectively increases under airflow acting force Dust migration velocity;Multiclass power supply integrated control system can control the different type power supply of each power supply zone simultaneously, set different Adjustment parameter, ensure efficiency of dust collection while save energy consumption;Outlet dust collect plant collects screening electric field by setting groove type plate The fraction Charged of 5 escapes.
The present apparatus has the characteristics that:1) can ensure flue-gas temperature deep-graded cooling (smoke temperature reducer one-level cooling, Flue gas humidity control device two level cools), dust, which is modified, improves efficiency of dust collection (ratio resistance reduces, adhesion increase), and dust classification is gone Except (import loudspeaker water conservancy diversion dust collect plant one-level removes the big dust of adhesion, conventional electric field two level removes most of dust, screening Electric field removes ultra-fine grain dust), the flue gas for sieving electric field passes perpendicularly through negative electrode steel wire and anode steel wire, avoids rapping Reentrainment of dust, effectively increase dust migration velocity;
2) flue gas is down to 80 DEG C by smoke temperature reducer and flue gas humidity control device, effectively by the SO in flue gas3Condensation Product dew, and neutralized by dust surface alkalinty oxide, it is stripped of downstream (NH4)2SO4The reactant SO of formation3, so that coal-fired The granular material discharged important component SO of power-plant flue gas3(condensable particulate matter) and (NH4)2SO4(droplet containing soluble salt) obtains Effective removal, greatly improves system particles thing removal efficiency, is provided for stable realize of coal-burning power plant particulate matter minimum discharge Precondition.
3) psychrometric means is adjusted by flue gas, the humidity of flue gas regulation is usually the increase on the basis of former smoke moisture 0.1%-0.5%, desulfurization wastewater or wet electrical dust precipitator waste water are sprayed into before electric cleaner (after smoke temperature reducer) in flue, For wastewater treatment capacity in 15t/h-50t/h, waste water obtains mass efficient processing;Accordingly, due to flue gas powder after flue gas water spray damping The increase of dirt adhesion, efficiency of dust collection effectively improve;Realize at the same adjust electric cleaner import smoke moisture and temperature with Dust collection efficiency is improved, reduces energy consumption.
4) import loudspeaker water conservancy diversion dust collect plant is stripped of because of smoke temperature reducer and flue gas humidity control device by setting electric field Set and the higher dust of caused adhesion, improve dust collection efficiency;Water conservancy diversion collecting plate set rapping apparatus, solve because Deflector dust stratification and blockage problem caused by decreasing temperature and increasing humidity.
Specific embodiment of the utility model is the foregoing is only, but the technical characteristics of the utility model is not limited to This, any those skilled in the art in field of the present utility model, all cover in this practicality newly by the change or modification made Among the scope of the claims of type.

Claims (15)

1. a kind of regulating temperature and humidity sieves electric cleaner, it is characterised in that:Including smoke temperature reducer (1), the flue gas being sequentially connected Humidity control device (2) and electric dust collector, along flow of flue gas direction, the electric dust collector includes import loudspeaker (3), routine successively Electric field (4), screening electric field (5) and outlet loudspeaker (6), the import loudspeaker (3) are interior to be provided with water conservancy diversion dust collect plant (7).
A kind of 2. regulating temperature and humidity screening electric cleaner as claimed in claim 1, it is characterised in that:Each import loudspeaker (3) four cathode hangers are equipped with, four cathode hangers connect a high voltage power supply;The conventional electric field (4) includes At least one electric precipitation room, four cathode hangers are provided with each electric precipitation room, and four cathode hangers connect a high pressure Power supply;The screening electric field (5) includes at least one screening electric precipitation room, eight the moon being provided with each screening electric precipitation room Pole is hung, and eight cathode hangers connect a high voltage power supply.
A kind of 3. regulating temperature and humidity screening electric cleaner as claimed in claim 1, it is characterised in that:Screening electric field (5) bag Negative pole part (8) and anode portion (9) are included, the negative pole part (8) and anode portion (9) are steel wire, the negative pole part (8) and anode Portion (9) is vertical with flue gas flow direction.
A kind of 4. regulating temperature and humidity screening electric cleaner as claimed in claim 3, it is characterised in that:Set on the negative pole part (8) There are some corona pins (10), the corona pin (10) includes screw and nut, and the tip of screw is away from negative pole part, the afterbody of screw It is fixed on by nut on negative pole part.
A kind of 5. regulating temperature and humidity screening electric cleaner as claimed in claim 3, it is characterised in that:The negative pole part (8) and sun The spacing in pole portion (9) is 400-500mm, and steel wire net height is 2000mm, and steel wire width is 1000mm, is on steel wire 8mm × 8mm square hole.
A kind of 6. regulating temperature and humidity screening electric cleaner as claimed in claim 3, it is characterised in that:In the screening electric field (5) The negative pole part (8) of each power supply zone by framework composition together, often arrange independent into one group by the anode portion (9).
A kind of 7. regulating temperature and humidity screening electric cleaner as claimed in claim 1, it is characterised in that:The water conservancy diversion dust collect plant (7) deflector (12), anode dust-collecting mechanism and negative electrode dust-collecting mechanism are included, by flow of flue gas direction, deflector (12) position In the upstream of anode dust-collecting mechanism and negative electrode dust-collecting mechanism.
A kind of 8. regulating temperature and humidity screening electric cleaner as claimed in claim 7, it is characterised in that:The negative electrode dust-collecting mechanism bag Cathode frame (13), cathode rapping axle (14) and cathode rapping motor (15) are included, cathode line is provided with the cathode frame (13) Or negative electrode steel wire, often arrange cathode frame (13) top and hung over by insulated hanging pole in import loudspeaker (3), neighbouring cathode framework (13) bottom is fixedly connected, and position corresponding with often arranging cathode frame (13) is provided with beater, institute on cathode rapping axle (14) State cathode rapping axle (14) with cathode rapping motor (15) to be connected, the cathode rapping motor (15) is fixed on import loudspeaker (3) Top.
A kind of 9. regulating temperature and humidity screening electric cleaner as claimed in claim 8, it is characterised in that:The anode dust-collecting mechanism bag Anodic porous plate (16) and cathode vibrator are included, anodic porous described in a row is provided between two adjacent row's cathode frames (13) Plate (16), the level height of anodic porous plate (16) bottom are more than the level height of cathode frame (13) bottom, and anode shakes Beating device includes anode electric motor of shaker (17) and anode rapping shaft (18), on anode rapping shaft (18) and often row's anodic porous plate (16) position corresponding to is provided with beater, and the anode rapping shaft (18) is connected with anode electric motor of shaker (17), and the anode shakes Beat the bottom that motor (17) is fixed on import loudspeaker (3).
A kind of 10. regulating temperature and humidity screening electric cleaner as claimed in claim 9, it is characterised in that:The anodic porous plate (16) the left and right sides is provided with the bevelling (19) that flue gas is imported to anodic porous plate (16), is provided with the anodic porous plate (16) Equally distributed through hole (20).
A kind of 11. regulating temperature and humidity screening electric cleaner as any one of claim 7 to 10, it is characterised in that:It is described The flow distribution plate (21) for spreading flue gas to surrounding is equipped with deflector (12), anode dust-collecting mechanism and negative electrode dust-collecting mechanism.
A kind of 12. regulating temperature and humidity screening electric cleaner as claimed in claim 1, it is characterised in that:The flue gas humidity control device (2) water-supply-pipe (23) being arranged in flue (22) is included, the end of the water-supply-pipe (23) is provided with nozzle (24), the nozzle (24) just it is staggered, nozzle (24) sprays flow direction and flow of flue gas is reversely consistent.
A kind of 13. regulating temperature and humidity screening electric cleaner as claimed in claim 12, it is characterised in that:The water-supply-pipe (23) is met Wind face is provided with abrasionproof angle steel.
A kind of 14. regulating temperature and humidity screening electric cleaner as claimed in claim 12, it is characterised in that:The water-supply-pipe (23) with Connected between water inlet manifold by transparent hose (27), the both ends of the transparent hose (27) are equipped with stop valve (28).
A kind of 15. regulating temperature and humidity screening electric cleaner as claimed in claim 1, it is characterised in that:In the outlet loudspeaker (6) Provided with dust collection plate (29), the dust collection plate (29) includes plate body (30), and plate body is provided with flue gas upstream at left and right sides of (30) The first side plate (31), the front end of every piece of first side plate (31) is provided with plate body (30) second side plate of center (32), two piece Fume inlet passage (33) is left between two side plates (32).
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108722668A (en) * 2017-04-14 2018-11-02 浙江菲达环保科技股份有限公司 A kind of regulating temperature and humidity screening electric precipitator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108722668A (en) * 2017-04-14 2018-11-02 浙江菲达环保科技股份有限公司 A kind of regulating temperature and humidity screening electric precipitator

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